US2581097A - Treatment of molten steel - Google Patents

Treatment of molten steel Download PDF

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US2581097A
US2581097A US161264A US16126450A US2581097A US 2581097 A US2581097 A US 2581097A US 161264 A US161264 A US 161264A US 16126450 A US16126450 A US 16126450A US 2581097 A US2581097 A US 2581097A
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sodium nitrate
heat
slag
steel
lime
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US161264A
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Frederick J Griffiths
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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/04Manufacture of hearth-furnace steel, e.g. Siemens-Martin steel

Definitions

  • This invention relates, as indicated, to the treatment of molten steel.
  • the process effects a reduction in the carbon content, and a slight reduction in the lp content of the steel, but little or no reduction in the silicon, since the effectiveness of the sodium nitrate is largely lost, due to the fact that it reacts with the ferrosilicon, which itself contains a large proportion of silicon and therefore the sodium nitrate has little or no effect in reducing the silicon content of the steel itself.
  • Attempts to reduce the sulphur content of the steel usually include the addition of large amounts of lime to the furnace to increase the basicity of the slag, so that the volume of slag is increased, and the effectiveness of the sodium nitrate-ferrosilicon mixture is further reduced.
  • the invention contemplatesa method of treating molten steel in an open hearth furnace, which is effective to produce a cleansteel, free from oxides and other impurities, with an increase in the yield of clean steel and a shortening in the time of production of each heat.
  • the invention further contemplates a method of treating molten steel, which involves a change of a physical nature in the shaping up of the slag, whereby the heat transfer to the metal bath is greatly accelerated, due to the use of sodium 9 Claims.
  • flush de signates a heat of steel to which ore additions have been made, as a result of which, a very large volume of slag is created, a portion of which is flushed or removed from the furnace in the course of making the heat of steel, whereas the term noneflush refers to a heat of steel, to which such ore additions have not been made, and which therefore does not require such flushing.
  • the making of the heat is continued in the usual manner, but no more sodium nitrate is added until the heat is ready to be shaped up and the slag conditioned.
  • the sodium nitrate is preferably added when the fuel is off and the furnace is being reversed, the fuel being left 011 until the addition of sodium nitrate is completed The heat is then continued in the usual way, and the furnace tapped.
  • the addition of the sodium nitrate to the undissolved lime causes a generation of heat, and also causes the lime to dissolve, forming a eutectic of a higher lime-silica ratio.
  • This higher limesilica ratio which is considerably in excess of 2.8:1, has a higher saturation value for the transfer of sulphur into the slag, with the resultthat the sulphur content of the steel is rapidly reduced.
  • the carbon and silicon contents are also reduced rapidly, since the effectiveness of the sodium nitrate is not lost by reason of the fact that it is required to react exothermically with ferrosilicon.
  • the tonnage of steel produced per hour is increased, the sulphur content of the steel is lowered, and a cleaner steel, in general, is obtained.
  • the process saves money on fluxes, because for every pound of sodium nitrate which is used, two to three pounds of fluorspar are saved.
  • sodium nitrate is added to the heat, 200 pounds at a time, at least 500 pounds being added, until the lime boil is started, after which no further addition is made.
  • the amount of sodium nitrate used depends upon the silicon content of the iron, the higher the silicon content, the greater the amount of sodium nitrate used. This procedure produces a desired high temperature, saves considerable time in the production of the heat, and gives a lower sulphur melt.
  • the making of the heat is continued in the usual manner, but no more sodium nitrate is added until the heat is ready to be shaped up and the slag conditioned.
  • the sodium nitrate is preferably added when the fuel is off and the furnace is being reversed, the fuel being left off until the addition of sodium nitrate is completed.
  • the improvement in a method of producing increasing the temperature of the bath, thereby aiding in transfer of heat through the slag to the additions of fiuorspar are made to the furnace slag after the slag has been conditioned.
  • sodium nitrate being about 5 to 2.

Description

Patented Jan. 1, 1952 UNITED/STATES PATENT OFFICE 2,581,097 TREATMENT or MOLTEN STEEL Frederick J. Grifl'iths, Massijlon, Ohio No Drawing. Application May 10, 1950,
Serial No. 161,264
This invention relates, as indicated, to the treatment of molten steel.
In my U. S. Patent No. 2,446,759, I have disclosed an open-hearth process in which a layer of slag comprising calcium gxide and iron oxide is formed on a bath of molten steel in an open hearth furnace, and an exothermic reaction mixture consisting of sodium nitrate and ferrosilicon is ignited in contact with the slag, thereby producing sodium oxide capable of reacting with one or more components of the slag to modify the characteristics of the slag and promote a reaction between carbon contained in the steel and iron oxide contained in the steel and slag.
The process effects a reduction in the carbon content, and a slight reduction in the lp content of the steel, but little or no reduction in the silicon, since the effectiveness of the sodium nitrate is largely lost, due to the fact that it reacts with the ferrosilicon, which itself contains a large proportion of silicon and therefore the sodium nitrate has little or no effect in reducing the silicon content of the steel itself.
Attempts to reduce the sulphur content of the steel usually include the addition of large amounts of lime to the furnace to increase the basicity of the slag, so that the volume of slag is increased, and the effectiveness of the sodium nitrate-ferrosilicon mixture is further reduced.
Aside from the foregoing disadvantages, there is a further disadvantage in that the total time for producing a heat of steel, having a desired low content of sulphur, carbon and silicon, is not reduced to any great extent over normal practice, when using such exothermic reaction mixtures.
I have discovered, as the result of a series of tests, both experimentally, and in actual production, that I can effect a rapid and better controlled reduction in the carbon, silicon and sulphur contents of the steel, particularly sulphur, by adding sodium nitrate alone to the furnace, in relatively large amounts, depending upon the silicon content of the steel.
The invention contemplatesa method of treating molten steel in an open hearth furnace, which is effective to produce a cleansteel, free from oxides and other impurities, with an increase in the yield of clean steel and a shortening in the time of production of each heat.
The invention further contemplates a method of treating molten steel, which involves a change of a physical nature in the shaping up of the slag, whereby the heat transfer to the metal bath is greatly accelerated, due to the use of sodium 9 Claims. (01, 7 555 nitrate, which is used directly on the undissolved lime or in conjunction with calcium fluoride, to form a mixture or solution of a eutectic nature, 1. e., having a low melting point, which facilitates transfer of heat to the molten steel, and produces a desired cleaning action on the steel.
The procedure, and the time of addition of the sodium nitrate varies somewhat, depending upon whether a flush or non-flush heat of steel is being produced. The term flush de signates a heat of steel to which ore additions have been made, as a result of which, a very large volume of slag is created, a portion of which is flushed or removed from the furnace in the course of making the heat of steel, whereas the term noneflush refers to a heat of steel, to which such ore additions have not been made, and which therefore does not require such flushing. When a flush heat is being made, after the flushing, a large portion of the silica is removed incidental to the flushing operation, so that the heat is in what may be termed an endothermic condition, the temperature of the metal being relatively low, so that a relatively great increase in temperature is required to continue the purifying of the metal.
In accordance with the invention, and assuming that a flush heat of steel is being produced in a ton open hearth furnace, when the heat is finishing flush, I add sodium nitrate to the heat, beginning with a 200 pound addition, and continuing, when necessary, to add sodium nitrate until a total of 500 pounds has been added. The reaction of the sodium nitrate with the lime increases the temperature to a desired point and saves considerable time in bringing the lime up from the bottom of the furnace. It brings the lime up quickly and in a relatively soft condition. The higher the silicon content of the heat, the greater the amount of sodium nitrate used. It is necessary to use enough sodium nitrate to bring the metal to a relatively high temperature. When the lime boil begins, no further additions of sodium nitrate are made until after the lime boil is completed.
The making of the heat is continued in the usual manner, but no more sodium nitrate is added until the heat is ready to be shaped up and the slag conditioned.
When the slag is ready to be shaped up, additions of fluorspar and sodium nitrate are made, 500 pounds of fluorspar being added for every 200 pounds of sodium nitrate, the fluorspar being first added by itself, and the heat being left undisturbed until the desired temperature is attained, and after about minutes at such temperature, the sodium nitrate is added.
The sodium nitrate is preferably added when the fuel is off and the furnace is being reversed, the fuel being left 011 until the addition of sodium nitrate is completed The heat is then continued in the usual way, and the furnace tapped.
The addition of the sodium nitrate to the undissolved lime causes a generation of heat, and also causes the lime to dissolve, forming a eutectic of a higher lime-silica ratio. This higher limesilica ratio, which is considerably in excess of 2.8:1, has a higher saturation value for the transfer of sulphur into the slag, with the resultthat the sulphur content of the steel is rapidly reduced. The carbon and silicon contents are also reduced rapidly, since the effectiveness of the sodium nitrate is not lost by reason of the fact that it is required to react exothermically with ferrosilicon.
Through the use of sodium nitrate at various times during the working of the heat, considerable time is saved, both in the faster dissolving of the lime into the slag and the preparation of a slag having a lime-silica ratio higher than is normally obtained.
The tonnage of steel produced per hour is increased, the sulphur content of the steel is lowered, and a cleaner steel, in general, is obtained.
The process saves money on fluxes, because for every pound of sodium nitrate which is used, two to three pounds of fluorspar are saved.
When non-flush heat is being produced, after the hot metal has been added to the furnace,
sodium nitrate is added to the heat, 200 pounds at a time, at least 500 pounds being added, until the lime boil is started, after which no further addition is made. The amount of sodium nitrate used depends upon the silicon content of the iron, the higher the silicon content, the greater the amount of sodium nitrate used. This procedure produces a desired high temperature, saves considerable time in the production of the heat, and gives a lower sulphur melt.
The making of the heat is continued in the usual manner, but no more sodium nitrate is added until the heat is ready to be shaped up and the slag conditioned.
When the slag is ready to be shaped up, additions of fluorspar and sodium nitrate are made, 500 pounds of fluorspar being added for every 200 pounds of sodium nitrate, the fluorspar being first added by itself and the heat being left undisturbed until the desired temperature is attained, and after about ten minutes at such temperature, the sodium nitrate is added.
The sodium nitrate is preferably added when the fuel is off and the furnace is being reversed, the fuel being left off until the addition of sodium nitrate is completed.
The following are examples of heats produced in accordance with the invention:
HEAT 5627 Furnace charge:
Pig iron 4,300 Car wheels 54,050 Molds 24,800 Borings iron 15,000 Crops 78,700 #2 Hev melt 66,050 Turnings 96,750 Pit scrap 11,400 Burnt lime 16,200
Ladle additions: 70# AL 1050# Reg. FeMn 600# L. C. FeMn Mold addition-484% AL Other details:
Yield, 88.7% Net tons, 159.4 N/T per hr. T-T, 9.96 16 hrs. tap-tap, 1:30 Int. '75-17 17 64-318,750
Analysis in percent 8:50 a. m 4004* NaNOs 9:10 3000# burnt lime 9:1'7/20 Oxygen 9:45 Lab .074 sulphur 9:50 200# NaNOs 400a spar 10:10 1000# spar 500# roll scale 10:35 1500# burnt lime 10:55 Lab .046 sul.
11:05 3000# pig iron 11:20 300# spar 40()# roll scale 11:50 .033 sul.
12:00 noon 3000# burnt lime 12:15 p.m 200# rim flux 100# NaNO: 12:20/26 Oxygen 1 Tap Rim fiat to center Good grade burnt lime HEAT 5633 Furnace charge:
Pig iron 22,500 1343 skull 48,250 Wheels 12,600 Crops 70,550 #1 steel 50,950 #2 Hev melt 81,550 Turnings 42,650 Burnt lime 16,850
Ladle additions: AL 1150# FeMn 600# L. C. Mn Mold addition-35# Other details:
Yield, 85.2 Net tons, 148.7 N/T per hr. T-T, 11.01 13:30 tap-tap, 1:00 Int. -17x1'7x64-297,500
Analysis in percent 0 Mn Phos Sul Gr Ni Mo Sn Cu It is apparent from the foregoing examples that the sulphur is rapidly reduced during the mixtures of the character described.
Having thus described my invention, I claim: 1. The improvement in a method of producing increasing the temperature of the bath, thereby aiding in transfer of heat through the slag to the additions of fiuorspar are made to the furnace slag after the slag has been conditioned.
to sodium nitrate being about 5 to 2.
4. The method, as defined in claim 3, in which the additions of sodium nitrate are made at those intervals when the furnace is being reversed and the fuel is off.
5. The improvement in a method of producing steel in an open hearth, which comprises form- 8. The improvement in a method of producing steel in an open hearth, which comprises forming a bath of slag-covered molten metallic iron FREDERICK J. GRE'FITHS.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 94,995 Bessemer Sept. 21, 18-69 594,497 Stockman Nov. 30, 1897 1,997,602 Robinson Apr. 16, 1935 2,446,759 Grifliths Aug. 10, 1948 OTHER REFERENCES Metal Progress, December 1947, page 966. Published by the American Society for Metals, Cleveland, Ohio.

Claims (1)

1. THE IMPROVEMENT IN A METHOD OF PRODUCING STEEL IN AN OPEN HEARTH FURNACE WHICH COMPRISES FORMING BATH OF MOLTEN METALLIC IRON IN THE FURNACE HAVING A LAYER OF A LIME SLAG THEREON, AND ADDING SODIUM NITRATE ALONE ONTO THE SLAG, THE REACTION OF THE SODIUM NITRATE WITH THE LIME INCREASING THE TEMPERATURE OF THE BATH, THEREBY AIDING IN TRANSFER OF HEAT THROUGH THE SLAG TO THE MOLTEN IRON, AND AIDING IN STARTING THE LIME BOIL.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US94995A (en) * 1869-09-21 Improvement in the mawdtactttre of iron and steel
US594497A (en) * 1897-11-30 Process of purifying iron
US1997602A (en) * 1932-03-10 1935-04-16 Frank S Christy And Nanette Ch Process of refining molten metal
US2446759A (en) * 1945-10-22 1948-08-10 Chromium Mining And Smelting C Open-hearth process

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US94995A (en) * 1869-09-21 Improvement in the mawdtactttre of iron and steel
US594497A (en) * 1897-11-30 Process of purifying iron
US1997602A (en) * 1932-03-10 1935-04-16 Frank S Christy And Nanette Ch Process of refining molten metal
US2446759A (en) * 1945-10-22 1948-08-10 Chromium Mining And Smelting C Open-hearth process

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